EP2990378B1 - Composants de zéolite destinés à être utilisés dans des générateurs d'oxygène chimique solide - Google Patents

Composants de zéolite destinés à être utilisés dans des générateurs d'oxygène chimique solide Download PDF

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EP2990378B1
EP2990378B1 EP14182423.5A EP14182423A EP2990378B1 EP 2990378 B1 EP2990378 B1 EP 2990378B1 EP 14182423 A EP14182423 A EP 14182423A EP 2990378 B1 EP2990378 B1 EP 2990378B1
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oxygen
composition
decomposition
zeolites
zeolite
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EP2990378A1 (fr
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Christoph Kallfass
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Diehl Aviation Gilching GmbH
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Diehl Aviation Gilching GmbH
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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02—Preparation of oxygen
    • C01B13/0203—Preparation of oxygen from inorganic compounds
    • C01B13/0218—Chlorate
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J7/00—Apparatus for generating gases
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02—Preparation of oxygen
    • C01B13/0296—Generators releasing in a self-sustaining way pure oxygen from a solid charge, without interaction of it with a fluid nor external heating, e.g. chlorate candles or canisters containing them

Definitions

  • the present invention relates to solid compositions for generating oxygen, suitable for use in an oxygen candle, the composition comprising at least one oxygen source selected from alkali metal chlorates, alkali metal perchlorates, alkaline earth metal chlorates, alkaline earth metal perchlorates and mixtures thereof, to oxygen generators comprising such compositions, to methods for generating oxygen by combusting such compositions, and to the use of zeolite compounds comprising at least one transition metal as a constituent of the framework as multifunctional components in such compositions.
  • compositions for generating oxygen are required in restricted environments such as submarines or space capsules, or in emergency situations such as in case of sudden pressure drops in aircrafts.
  • oxygen generating compositions are known since a long time.
  • the compositions produce oxygen by thermal decomposition of alkali metal chlorates or perchlorates or alkaline earth metal chlorates or perchlorates.
  • Accessory combustible materials such as carbon or metal powders (serving as fuels, i. e. reducing agents) may be added in order to assist in obtaining the high temperatures required for the decomposition of the chlorates and/or perchlorates.
  • the chlorates and/or perchlorates halogenates (+V, +VII)
  • the compositions are also called “oxygen candles” or "chlorate candles”.
  • binders or stabilizers such as silicates and mica (e.g. phlogopite), for influencing the decomposition rate of the oxygen sources and assisting in maintaining structural integrity, additives for suppressing undesired side reactions or for capturing undesired side products, and catalysts such as oxides of various transition metals for speeding up reaction rates or for lowering reaction temperatures, respectively.
  • compositions are molten and cast into a desired shape or, usually, press-moulded into powder compacts such as cylindrical rods, tablets, briquettes or other shapes.
  • the shaped composition is placed into a container, and combined with a primer to yield an oxygen generator, which ideally can be easily handled and stored for a quite long time without suffering deterioration.
  • the primer ignitionor
  • the released energy starts the halogenate decomposition reaction which proceeds without supply of auxiliary power.
  • the oxygen generators shall produce an oxygen stream reliably and continuously over an extended period of time.
  • the oxygen stream shall be breathable by humans, i. e. essentially free from toxic or otherwise noxious components such as carbon monoxide, carbon dioxide, and chlorine, and shall be provided at a temperature as close to room temperature as possible.
  • the oxygen generating composition Prior to and during the reaction, the oxygen generating composition should also be in a mechanically stable form in order to avoid any failure during activation (ignition) of the composition, and to avoid interruptions of the oxygen flow, which might result from mechanical alterations of the composition structure induced by external influences, or by modifications of the course of reaction.
  • the candle may melt not only in the reaction zone, but also at some distance from the reaction zone. Thus, there is a liquid zone travelling through the candle upon decomposition.
  • binders such as mica, asbestos fibers, infusorial earth, silicious fillers, or fiberglass.
  • the binders also help to avoid extreme volume changes of the candles due to oxygen loss, which is particularly important if an oxygen generator does not contain one single candle, but a plurality of candles in contact with each other. In such an arrangement one burning candle ignits the next candle. Shrinkage of the burnt candle at least deteriorates contact and makes proper decomposition/combustion propagation impossible.
  • CN 1 035 248 A discloses a candle for oxygen generation comprising NaClO 3 and a catalyst (Co, Mn).
  • a catalyst Co, Mn
  • Kaolin and zeolites are disclosed.
  • the oxygen shall have a temperature as low as possible.
  • composition for generating oxygen the oxygen generator, the method for generating oxygen, and the use as claimed in the independent claims.
  • Embodiments of the invention are indicated in the respective dependent claims.
  • the oxygen generator of the invention is an apparatus comprising the composition for generating oxygen of the invention as well as other means and devices essential or advantageous for proper functioning, and conventional per se, for example a containment, an igniting device, means for heat insulation, filter layers for retaining particulates, etc.
  • a containment for example a containment, an igniting device, means for heat insulation, filter layers for retaining particulates, etc.
  • igniting device means for heat insulation, filter layers for retaining particulates, etc.
  • the oxygen generating composition of the present invention is typically provided in the form of powder compacts, such as press-moulded rods, pellets, sheets, tablets and briquettes, however, the morphological shape and structure is not limited in any particular manner.
  • the composition may be formed into tablets having different oxygen production capacities achieved by zones of different reaction velocities as described in DE 37 25 105 A1 .
  • the tablets may be contained in the oxygen generator container in bulk form, and intimate contact between tablets may be maintained, for example, by a tension member such as a pressure spring.
  • the oxygen generating composition contains components conventional in such compositions, namely oxygen sources, and optionally fuels, and various auxiliary agents.
  • Oxygen sources are halogenates, i. e. chlorates, perchlorates, and mixtures of chlorates and perchlorates of alkali metals or alkaline earth metals or mixtures thereof.
  • the oxygen sources are chlorates and/or perchlorates of lithium, sodium, potassium, and mixtures thereof. Particularly preferred are chlorate and perchlorate of sodium. Sodium perchlorate is the most preferred oxygen source.
  • fuels various metals in powder form can be advantageously used.
  • the fuels act as reducing agents, and are oxidized to metal oxides, thus providing additional energy for supporting the decomposition.
  • Exemplary fuels are fine powders of aluminium, iron, magnesium, manganese, silicon, and titanium, and non-metals such as boron and carbon may also be used.
  • barium peroxide and the oxide, peroxide and hydroxide of alkali metals shall be specifically mentioned. These compounds serve for binding chlorine and carbon dioxide, which are sometimes produced in trace amounts, but should not be present in breathable oxygen.
  • the oxygen generating composition contains components, known per se, but not heretofore used in oxygen generating compositions.
  • the composition of the present invention contains a zeolite or a mixture of zeolites which replace, at least in part, conventional binders and catalysts.
  • the zeolites are multifunctional in that they serve both as binders and as catalysts. They contain at least one transition metal as a constituent of the framework.
  • the compositions do not contain any binders and/or catalysts in addition to the multifunctional components, although the presence of conventional binders, such as silicates or mica, and/or conventional catalysts, such as oxides of iron, cobalt or manganese, in addition to the multifunctional components, is not excluded.
  • Zeolites constitute a large family of compounds which can be classified on the basis of characteristic structural features into various groups. There exist several classification systems and criteria for distinguishing between the numerous zeolite types. However, all zeolites have many unique structural features in common allowing, for example, formation of continuous series of mixed crystals. As a consequence, the compounds belonging to the zeolite family behave similarly.
  • Zeolites occur naturally, and are also produced industrially on a large scale. Industrially important zeolites are produced synthetically, for example by sol-gel processing. While naturally occurring zeolites are rarely pure, synthetic zeolites are manufactured in a uniform, phase-pure state. It is also possible to synthesize zeolite structures which do not occur in nature. For the purposes of the present invention, both naturally occurring zeolites and synthetically produced zeolites are suitable, but synthetically produced zeolites are preferred.
  • Zeolites are microporous, crystalline aluminosilicates or alumosilicates, respectively, belonging to the tectosilicates.
  • the zeolite framework is built of corner-linked tetrahedra. Each tetrahedron consists of four oxygen ions which surround an Al ion or an Si ion.
  • the framework may also contain OH- and/or F-groups, which replace oxygen ions and belong to only one single tetrahedron.
  • some Al and/or Si ions may be replaced by different ions, for example ions of phosphorus; some Al and/or Si ions are replaced by transition metal ions.
  • the structures thus formed always comprise open channels. These open channels may form a one-dimensional system of channels (i.e. the channels are not connected to each other), a two-dimensional system of channels (i.e. the channels are connected in two dimensions), or a three-dimensional system of channels (i.e. the channels are connected in three dimensions).
  • Some zeolite types also comprise open and/or closed cages.
  • the zeolite framework is negatively charged, and positive ions are required to compensate for the negative charge.
  • Such ions are typically alkali metal ions or alkaline earth metal ions, for example Na + , K + , Ca 2+ or Mg 2 + . These ions are not constituents of the zeolite framework, but are rather accommodated within cavities, i.e. hollow spaces, of the framework. Cavities include open channels and open and closed cages.
  • Species accommodated within channels and open cages can move, and may be exchanged by different species, while species within closed cages remain fixed within the framework.
  • Zeolites have the empirical formula M n+ x/n (Al x Si y O 2 ) ⁇ zH 2 O
  • M is typically an alkali metal ion or an alkaline earth metal ion present in an amount as appropriate for compensating the anionic charge of the zeolite framework resulting from the replacement of silicon by aluminum.
  • n represents the charge of M, and is typically 1 or 2.
  • z indicates the number of water molecules contained within the zeolite crystal. The amount of water varies among different zeolite types, and also within one and the same zeolite because water can be absorbed and desorbed reversibly.
  • z may range from 0 to a number corresponding to up to about 40 weight% of a particular zeolite crystal.
  • Zeolites for use in the present invention preferably contain less water, e.g. up to about 20 weight % or less, and zeolites without crystal water may be advantageously used.
  • the zeolite compounds act as binders and facilitate the decomposition of alkali metal and alkaline earth metal chlorates and perchlorates, i.e. catalyse the decomposition of these halogenates.
  • they can replace both conventional binders and conventional catalysts at the same time.
  • a part of the aluminum and/or silicon ions of the zeolite framework is replaced by transition metal ions conventionally known to be catalytically active in oxygen candles.
  • Suitable metals are, in particular, iron, cobalt and manganese.
  • Such catalytically active constituents are included as constituents of the zeolite framework (i.e. replacing Al and/or Si) and may be, in addition, trapped within cages of the zeolite framework. The presence of such fixed catalytically active constituents further enhances the catalytic activity of the zeolites for generating oxygen.
  • Introduction of the catalytically active ions can be performed by known procedures, e.g. during preparation of the zeolite.
  • compounds conventionally known as "fuels” may be introduced into open channels and/or open cages of the zeolite framework.
  • Suitable compounds are, for example, transition metals like e.g. Fe, Mn, Ti, Zn, Cu, Zr, Co containing compounds or carbon containing compounds.
  • Such fuels which are movably incorporated, can be introduced by known procedures, e.g. via ion exchange or via adsorption. They act as reducing agents, and are oxidized during the decomposition reaction, thus providing additional energy for supporting the decomposition.
  • Zeolites having fuels releasably incorporated therein may replace, at least in part, not only binders and catalysts, but also conventional fuels, in an oxygen candle.
  • Examples for synthesizing transition metal containing zeolites are indicated e.g. in Rossin J. A. et al.: Synthesis of cobalt containing ZSM-5, Zeolites, 1987, 7, pp 295-300 ; Patarin J. et al.: Iron distribution in iron MFI-type zeolite samples synthesized in fluoride medium: Influence of the synthesis procedure, Zeolites, 1990, pp 674-679 ; Heinrich A. R.
  • Particularly preferred fuels are transition metal compounds which are oxidized into catalytically active transition metal oxides.
  • iron hydroxide FeOH shall be mentioned.
  • Iron hydroxide as a fuel is oxidized during the decomposition reaction into iron oxide Fe 2 O 3 , and iron oxide constitutes a catalyst for the chlorate/perchlorate decomposition reaction.
  • catalytic activity and fuel activity can be advantageously combined.
  • a further advantage of zeolites in compositions for generating oxygen stems from their reversible hydration/dehydration ability.
  • the transition from the hydrated to the dehydrated forms is an endothermic reaction. Consequently, at least some of the reaction heat released by a burning candle is used for providing the energy for the endothermic zeolite dehydration reaction.
  • the consumed heat is no longer available for heating the oxygen liberated from the oxygen candle, and, therefore, the oxygen is provided at a lower temperature than without use of the multifunctional zeolites of the present invention.
  • Excess water within the product gas can be captured by water absorption or filter means provided within the oxygen generator container, and conventionally known in the art.
  • Exemplary zeolites for use in the present invention are sodalites, mordenites, heulandites, and natrolites.
  • Sodalite is a zeolite without zeolitic water, and comprising cages. Sodalite has the chemical formula Na 8 [(Cl, OH) 2 Al 6 Si 6 O 24 ].
  • Mordenite has the chemical formula (Na 2 , Ca, K 2 ) 4 (Al 8 Si 40 )0 96 ⁇ 28H 2 O. Mordenite has a one-dimensional system of open channels.
  • Heulandite is a not specifically defined compound of a series of mixed crystals having the chemical composition (X) 5 [Al 9 Si 27 O 72 ] ⁇ ⁇ 24H 2 O.
  • X may be Ba, Ca, K, Na, and Sr, which may replace each other in the chemical formula.
  • Heulandite has a two-dimensional system of open channels.
  • Natrolite has the chemical formula Na 2 [Al 2 Si 30 O 10 ] ⁇ 2H 2 O. It is the Na-rich end member of a series of mixed crystals, wherein Na is replaced by Ca and water. The other end members are scolecite Ca[Al 2 Si 3 O 10 ] ⁇ 3H 2 O and mesolite Na 2 Ca 2 [Al 6 Si 9 O 30 ] ⁇ 8H 2 O. Natrolite has a three-dimensional system of open channels.
  • zeolites mentioned above are merely disclosed by way of example, but other zeolite types are suitable as well. Namely, although the family of zeolites is large, all zeolites behave substantially similar. It is believed that the similar behaviour of all compounds belonging to the zeolite family is due to the numerous structural similarities of these compounds (allowing, for example, the formation of continuous series of mixed crystals), in particular the framework structure having open cavities, resulting in similar properties and effects.
  • the multifunctional zeolite compounds used according to the present invention provide distinct advantages when incorporated into oxygen generating compositions.
  • the process of decomposition proceeds without formation of a liquid phase. That is, while a reaction zone travels through a "burning" candle, no liquid zone travels through the candle. Any localized melting of the composition cannot be observed.
  • Candles, or other shaped parts, according to the present invention are less susceptible to external influences, for example shocks, or shaking or tilting an oxygen generator during use. Separation of used portions from unused portions of a candle at their liquid interfaces is avoided due to a lack of such liquid interfaces, thus avoiding interruption of decomposition/combustion, and reliably providing a continuous and enduring oxygen flow.
  • the candles, or other shaped parts substantially maintain their sizes and shapes during use, although they release considerable amounts of their chemically bound oxygen, due to oxygen liberation in gaseous form. Therefore, while in prior art candles the morphological structure breaks down during use of a candle, i. e. the reaction residues have a remarkable smaller volume than the starting compositions, in candles according to the present invention the structure remains substantially intact. What can be observed is an increase of porosity: While a pristine candle may have no visible pores or only a few pores and/or small pores, a used candle is porous or, at least, has more pores and larger pores than a pristine candle.
  • the structural stability also reduces contact problems in oxygen generator embodiments using a series of candles, or candles (tablets, pellets) in bulk form.
  • the reaction starts at lower reaction temperatures than without catalyst, and produces less reaction heat than with prior art catalysts.
  • the oxygen liberated from the compositions of the present invention is at a somewhat lower temperature, and thus more suitable for physiological use.
  • the decomposition of the composition comprising sodium chlorate and cobalt oxide CoO starts at about 300°C, progresses quite quickly and in a constant manner with increasing temperature, and is completed at about 500°C. 50 weight% of the sodium chlorate have been decomposed at about 386°C.
  • the decomposition of the composition comprising sodium chlorate and phlogopite starts at about 370°C, is slow at the beginning, but accelerates with increasing temperature, and is completed at about 580°C. 50 weight% of the sodium chlorate have been decomposed at about 542°C.
  • the decomposition of the composition comprising sodium chlorate and mordenite or natrolite starts at about 300°C, proceeds slowly and with a constant rate until about 500°C, and proceeds quickly and with a constant rate at temperatures exceeding 500°C until completion of the decomposition at about 600°C. 50 weight% of the sodium chlorate have been decomposed at about 559°C.
  • the decomposition of the composition comprising sodium chlorate and sodalite starts at about 300°C, proceeds with an increasing rate until about 470°C and becomes somewhat slower at temperatures exceeding 470°C, until the decomposition is complete at about 600°C. 50 weight% of the sodium chlorate have been decomposed at about 500°C.
  • the decomposition of the composition comprising sodium chlorate and sodalite having iron within the framework starts at about 300°C, proceeds similar to the decomposition in the presence of unmodified sodalite (curve (e)), and is completed at about 600°C. 50 weight% of the sodium chlorate have been decomposed at about 489°C. It can be seen that the decomposition in the presence of iron-modified sodalite is shifted to somewhat lower temperatures as compared to unmodified sodalite.
  • the decomposition of the composition comprising sodium chlorate and sodalite having iron within the framework and within open cavities (i.e. containing a multifunctional component of the present invention; curve (g)) starts at about 300°C, proceeds quickly in the temperature range from about 350°C to 450°C, and then slows down until the decomposition is completed at about 582°C. 50 weight% of the sodium chlorate have been decomposed at about 424°C, and 75 weight% of the sodium chlorate have been decomposed at about 450°C.
  • Oxygen candles were prepared from all preparations described above with reference to Fig. 1 .
  • the constituents were milled, blended in a mixer, and then press-moulded into cylinders by applying a force from 40 to 400 kN involving post-compaction for a period between 1 to 5 minutes.
  • the obtained powder compacts were mechanically stable. They could be handled easily, and appeared to be poreless when observed with the naked eye.
  • the moulding pressure influenced the burning speed: Decomposition rate decreased with increasing moulding pressure, i.e.
  • powder compacts moulded with a pressure of 40 kN burned faster than powder compacts moulded with a pressure of 400 kN.
  • a moulding pressure in the range from 100 to 400 kN yielded powder compacts having a density of about 2.5 g/cm 3 , which appeared most suitable.
  • the oxygen candles were ignited by means of a conventional primer tablet.
  • the primer tablet provided the reaction heat for starting the decomposition reaction of the sodium chlorate, yielding sodium chloride and oxygen.
  • Fig. 2 powder diffraction patterns of a composition comprising sodium chlorate and natrolite, measured in situ at 600°C using a high temperature camera, are shown. The patterns were recorded in air using Cu-K ⁇ rays and a Ni-filter. Powder diffraction pattern A was recorded after the sample had been maintained at 600°C for one hour, and power diffraction pattern B was recorded after the sample had been maintained at 600°C for five hours.
  • This finding is used in the present invention for providing oxygen generators superior in resistivity against mechanical influences, and superior in reliability and endurance of oxygen formation. Even under adverse conditions such as vibrating environments or zero gravity oxygen is provided promptly and continuously.

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Claims (14)

  1. Composition pour générer de l'oxygène, adaptée pour utilisation dans une bougie à oxygène, la composition comprenant au moins une source d'oxygène choisie parmi des chlorates de métal alcalin, des perchlorates de métal alcalin, des chlorates de métal alcalino-terreux, des perchlorates de métal alcalino-terreux et des mélanges de ceux-ci,
    la composition comprenant en outre au moins un composé de zéolite, le composé de zéolite ayant une structure comprenant des canaux ouverts et, comprenant facultativement en outre des cages ouvertes et/ou des cages fermées, et le composé de zéolite comprenant au moins un métal de transition en tant que constituant de la structure.
  2. Composition selon la revendication 1, caractérisée en ce que l'au moins un composé de zéolite est choisi dans le groupe constitué de zéolites ayant un système de canaux unidimensionnel, zéolites ayant un système de canaux bidimensionnel, zéolites ayant un système de canaux tridimensionnel et zéolites ayant des cages.
  3. Composition selon la revendication 1 ou 2, caractérisée en ce que l'au moins un composé de zéolite est choisi dans le groupe de la mordénite, le groupe de l'heulandite, le groupe de la natrolite ou le groupe de la sodalite.
  4. Composition selon l'une quelconque des revendications 1 à 3, caractérisée en ce que l'au moins un composé de zéolite comprend au moins un métal de transition enfermé dans une cage fermée.
  5. Composition selon l'une quelconque des revendications 1 à 4, caractérisée en ce que l'au moins un composé de zéolite comprend au moins un composé contenant un métal de transition ou un composé contenant du carbone logé dans un canal ouvert et/ou dans une cage ouverte.
  6. Composition selon l'une quelconque des revendications 1 à 5, caractérisée en ce que le métal de transition est choisi dans le groupe constitué du fer, du manganèse, du cobalt, du zirconium, du zinc, du cuivre et du titane.
  7. Composition selon l'une quelconque des revendications 1 à 6, caractérisée en ce qu'elle comprend en outre au moins un combustible.
  8. Composition selon l'une quelconque des revendications 1 à 7, caractérisée en ce qu'elle comprend en outre au moins un agent auxiliaire adapté pour supprimer les réactions secondaires indésirables ou pour capturer les produits secondaires indésirables.
  9. Générateur d'oxygène comprenant une composition pour générer de l'oxygène par une décomposition autoentretenue, un récipient pour contenir la composition de génération d'oxygène, et un initiateur pour démarrer la décomposition de la composition de génération d'oxygène, caractérisé en ce que la composition de génération d'oxygène est une composition selon l'une quelconque des revendications 1 à 8.
  10. Générateur d'oxygène selon la revendication 9, caractérisé en ce que la composition est sous la forme d'une ou plusieurs pièces formées.
  11. Générateur d'oxygène selon la revendication 9 ou 10, caractérisé en ce que la composition est sous la forme d'une bougie à oxygène unique, d'une pluralité de bougies à oxygène agencées en série, ou d'une charge comprimée sous forme de vrac.
  12. Utilisation d'un composé de zéolite tel que défini dans l'une quelconque des revendications 1 à 6, en tant que composant multifonctionnel dans une composition pour générer de l'oxygène adaptée pour utilisation dans une bougie à oxygène, la composition comprenant au moins une source d'oxygène choisie parmi des chlorates de métal alcalin, des perchlorates de métal alcalin, des chlorates de métal alcalino-terreux, des perchlorates de métal alcalino-terreux et des mélanges de ceux-ci, dans laquelle le composant multifonctionnel est multifonctionnel en ce qu'il agit à la fois en tant que liant et facilite la décomposition de la source d'oxygène.
  13. Utilisation selon la revendication 12, caractérisée en ce que le composant multifonctionnel est en outre multifonctionnel en ce qu'il agit en tant que combustible en comportant des combustibles incorporés de façon réversible dans celui-ci.
  14. Procédé pour générer de l'oxygène par décomposition d'une composition comprenant au moins un source d'oxygène choisie parmi des chlorates de métal alcalin, des perchlorates de métal alcalin, des chlorates de métal alcalino-terreux, des perchlorates de métal alcalino-terreux et des mélanges de ceux-ci, caractérisé en ce que la fusion ou la fusion localisée de la composition pendant la décomposition est évitée en ajoutant au moins un composé de zéolite tel que défini dans l'une quelconque des revendications 1 à 6.
EP14182423.5A 2014-08-27 2014-08-27 Composants de zéolite destinés à être utilisés dans des générateurs d'oxygène chimique solide Active EP2990378B1 (fr)

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US14/837,568 US10207925B2 (en) 2014-08-27 2015-08-27 Zeolite components for use in solid chemical oxygen generators

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CN107462596A (zh) * 2017-08-08 2017-12-12 华侨大学 一种膨胀型防火涂层隔热性能实验装置
CN108083234B (zh) * 2017-12-29 2020-11-13 陕西斯达防爆安全科技股份有限公司 一种氧烛药
EP3604213B1 (fr) 2018-07-30 2020-09-30 Diehl Aviation Gilching GmbH Phyllosilicates modifiés destinés à être utilisés dans des compositions de génération d'oxygène chimique solide
US11641023B2 (en) 2020-04-07 2023-05-02 Hamilton Sundstrand Corporation Fuel cell system and method

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US10207925B2 (en) 2019-02-19
EP2990378A1 (fr) 2016-03-02

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